Apparatus for canning



Aprll Z9, Q o BALLv APPARATUS FOR CANN'ING Filed D80. 27, 1937 9 Sheets-Sheet 1 INVENTOR. I a. M BY 3 Q I M 5/. ATTORNEYS b April 29, 1941. c. 0. BALL 2,239,690

APPARATUS FOR CANNING Filed Dec. 27, 193v 9 Sheets-Sheet 2 INVENTOR. m 6 M,

ATTORNEY5 April 29, 1941. c O BALL 2,239,690

APPARATUS FOR CANNING Filed 1:90.. 27, 193"! 9 Sheets-Sheet s IN VEN TOR. m M

BY M w. ATTORNIY5 April 29, 1941. c. 0. BALL APPARATUS FOR CANNING Filed Dec. 27, 1937 9 Sheets- Sheet 4 R m w w ATTORNEY$ April 29,, 1941. c. 0. BALL APPARATUS FOR CANNING Filed Dec. 27, 1937 9 Sheets-Sheet 5 INVENTOR. m QM BY M I 6 v ATTORNEYv A ril 29, 1941. c, 0, BALL 2,239,690

APPARATUS FOR CANNING Filed Dec. 27, 19:57 9 Sheets-Sheet 7 -e b I A -5/ I} 55 i 52 i |I Irrn ATTORNEYS April 29, 1941.

c. 0. BALL 2,239,690

APPARATUS FOR CANNING Filed Dec. 27, 1937 9 Sheets-Sheet 8 April 29, 1941. c. 0. BALL APPARATUS FOR CANNING 9 Sheets-Sheet 9 ZW BY 3 [Q f ATTORNEY-5.

Filed Dec. 27, 1937 Patented Apr. 29, 1941 APPARATUS FOR CANNING Charles 0. Ball, Oak Park, Ill., assignor to American Can Company, New York, N. Y., a corporation of New Jersey 7 Application December 27, 1937, Serial No. 181,944

14 Claims.

The present invention relates to a method of canning food products and to an apparatus for carrying out the method steps, and has particular reference to-a continuous sequence of operations in a food canning method by means of which the food product is completely and quickly sterilized, cooled, filled into sterilized cans and heremetically sealed under sterile and sterilizing conditions.

An object of the invention is the provision of with the food being handled, such parts bein i cleaned and sterilized with each use.

an improved sterilizing method of canning food products and of an apparatus for canning the same in a short period of time and under conditions that insure full and complete sterilization without change of taste or other characteristics of the food and which prevent contamination or 'recontamination throughout the various stages of the process.

A further object is the provision of such a canning method and apparatus by means of which the food product is first sterilized, the sterilized product is then cooled and following this it is filled into cans which have been sterilized, the filled cans then being hermetically sealed with can covers which have been sterilized, all of the steps being coordinated to insure a rapid and uninterrupted procedure.

Another object is the provision of a canning method in which a. quantity of the product just sufiicient to fill a single can is segregated from a mass of the product and the segregated charge is then subjected to sterilizing heats under progressively increased pressures accompanied by progressively increased temperatures.

Yet another object of the invention is the provision of a method of sterilization of a food product in batches by subjecting the same to high temperatures of steam under pressure while confining the product within a sealed enclosure.

A further object is the provision of a. method of canning a food product in a cycle or series of connected steps which include sterilizing an empty can and sterilizing a predetermined quantity of the product with or without a liquid and then filling the sterilized product into the sterilized can and further adding a. sterilized brine or. other additional flavoring liquid or other substance if. desired and hermetically sealing the filled can by utilizing a sterilized can cover, all of the operations being performed without subjecting cans, covers, or can contents to recontamination at any stage.

Yet another object in such a sterilization method has to do with prevention of contamination of any apparatus parts coming in contact Another object of the invention is the provision of an improved sterilizing method of the character described in which the sterilized product prior to filling into the can is held under a vacuum. and during that time is protected from bacterial contamination.

An additional object is the provision of an apparatus for canning a food product which is capable of sterilizing an empty can, sterilizing a predetermined quantity of the product in different stages, and then filling the sterilized product into the sterilized can.

Numerous other objects and advantages of the invention will be apparent as it is better understood from the following description, which,

taken in connection with the accompanying drawings, discloses a preferred embodiment thereof. I

Referring to the drawings:

Figure l is a plan view of an apparatus embodying the invention and one for carrying out the steps of the method, parts being broken back in difierent places and at different levels to more clearly illustrate certain of the operations;

Fig. 2 is an enlarged sectional view taken substantially along the line 2-2 in Fig. 1 showing one unit on one side of the machine;

Fig. 3 is a schematic plan of the lower part of the machine as it would appear if viewed along the broken line designated as 3-3 in Fig. 2, showing by means of cam tracks, grooves, ports, etc., the sequence of certain of the operations'of the machine throughout one cycle;

Figs. 4 and 5 are similar plan views of the center part of "the machine showing certain pipe connections and associated grooves, being taken at difierent levels indicated respectively by the lines 4-! and 5-5 in Fig. 2;

Fig. 6 is a schematic plan of the upper part of the machine as taken along an imaginary course indicated by the broken line 66 in Fig.

2 showing only the central portion of the ma.- chine and suggesting the order of operation of some of the steps of the method;

Figs. '7, 8, 9, 10' and 11 are sectional views similar to Fig. 2 showing one unit as itwould ap-.

pear in its different positions throughout the operation cycle, the sections being taken substantially along the respective section lines 1-1,

H, 9-9, Ill-l0 and Il- -|l in Fig. 1;

Fig. 12 is a plan sectional view-taken substantially along the section line l2-I2 in Fig. -2; and

Fig. 13 is a schematic plan sectional view taken substantially along the line i3-i3 in Fig. 2 and showing certain steam and water pipe connections and associated grooves.

The invention contemplates a substantially continuous process of sterilizing a food product which may be of the discrete particle type such as .a whole grain corn, peas, diced carrots, beets,

beans or similar materials and this is done by treating a quantity of the product in batches.

In the more detailed description which fol.- lows there is given as an example one way of carrying out the method steps. In this example the canning of corn is selected and is treated in minimum batch form, that is, each batch is sufficient for one can and is separately treated. Obviously a batch could include sufficient corn to fill several cans. Each single can batch when sterilized and cooled is immediately filled into a can which has just been made sterile. The can is hermetically sealed in the least possible time.

Where the larger batch of product is treated an additional step relating to the dividing of the batch into smaller units before filling into individual cans will be necessary. Ordinary filling machines properly protected against contamination and. sealed against atmosphere will answer such purposes and will not be further discussed as such change in procedure will be obvious to one skilled in the art.

From the time a batch of material is segregated from the mass or supply of such material until it is finally sealed in the can it is confined out of communication and is cut off from the atmosphere and is held under various pressures depending upon the particular step in this cycle treatment. 'It is also treated throughout the process under sterileconditions and a cardinal principle which is followed in the treatment in the prevention of contamination at each and every sta e of operation.

Considered from the standpoint of the product,

'will be made to briefly bring out this simultaneous treatment by digression at certain parts of the main description which will proceed with the minimum interruption from the segregating of the single can batch of corn from the supply reservoir through to its final hermetic closure within the can.

The drawings illustrate an organized apparatus for carrying out the invention in a preferred series of method steps and on a food product such as whole grain corn. In the exemplification here- I in illustrated and described a hopper a. (Fig. 2) is moved under and is filled with the corn which is contained within a supply reservoir 1), (see also Fig. 8). The reservoir may be closed at the topbut is not airtight. This hopper when ready to receive the single can batch has already been cleaned and steam treated. The cleaning of the hopper will be fully considered at a later time.

During the filling of the hopper low pressure steam is caused to pass up from below and this steam continually flows through and around the food particles which are then entering into and around those which are already in the hopper as well as through the supply mass in the reservoir. Since the corn in the reservoir is not hot there will be little need for venting of the steam. However, Venting may take place around the sides of the loosely fitting reservoir cover. The filling of the hopper with its predetermined quantity or single can catch is shown in Fig. 8.

The hopper a when filled is cut off from the supply reservoir b being moved so that its top is out of alignment with the filling hole of the reservoir. Provision is made, however, for steam to continue to pass up through the hopper and to escape from above, this time by way of a channel which has no connection with the reservoir. This may be said to be the beginning of the sterilization of the batch of corn in the hopper and the degree of sterilization will depend upon the temperature of the steam used at that time and necessarily such steam will be under a pressure. The steam treatment of the corn while in the hopper is shown in Fig. 2 and requires a substantial time, somewhat less than half of the entire process, as will be more definitely pointed out hereinafter.

A perforated'hopper or sieve plate 0 provides the bottom for the hopper during the time the hopper is being filled and also while the steam is subsequently circulating through the charge of corn within the hopper. It is through the perforations of this plate that the low pressure steam enters the hopper.

The filled hopper, after its steam treatment, is next moved away from the perforated plate c and is brought over the top of and in alignment with a filling tube d. During this hopper transfer steam ceases to flow into the hopper from the perforated plate 0. The corn now discharges by gravity into the tube and at the same time steam passes up from the bottom of the tube and flows through the descending corn. The steam escapes into an upper chamber e adjacent to the reservoir b. Fig. 7 shows the passage of food from hopper to tube.

Filling tube at is partially or fully closed-at its bottom by a perforated tube slide j and it is through the perforations of this slide that the low pressure steam enters the bottom of the tube. The major part of the sterilization of the corn takes place while in the filling tube d and is carlied on in stages, this phase of treatment consuming about one-seventh of the timeof the total cycle of the entire treating process as will be hereinafter more fully explained.

Leaving for the present this feature of operations on the segregated chargeof corn now in the filling tube, consideration will first be given to steps which take place relative to the empty hopper a. It will be understood, however, that the operations on the corn in the filling tube continue without interruptions.

While the hopper is discharging the corn into the filling tube d a cleaning operation is taking place on the perforating hopper sieve plate 0. This cleaning of the perforated plate 0' is shown in Fig. 7 and will first be considered.

A pin cleaning device g is used for this purpose. This device includes a plurality of pins, one for each perforation. These pins are mounted upon a movable member. The pins are normally out. of and spaced below the perforations of the sieve openings of ,the hopper plate 0 but are in vertical alignment therewith at all times. The pins are in their normal position when the hopper is being filled with corn from the reservolr b (Fig, 8).

acsaeoo It is while the hopper is in position over the filling tube d as has just been described that the pins of the cleaning device a are'raised and pushed through the perforations of the plate c (Fig. 7). This action tends to force .out any food particles that may have lodged in the perforations. During this cleaning step of punching out the sieve openings steam under pressure is supplied to the space below the sieve openings of the plate and this steam escapes upwardly through the openings'following which water and then a mixture of steam and water is caused to flush I through the perforations and to carry out any food particles which are pushed up through the sieve openings. 1

Following the cleaning of the plate c the empty hopper a is moved away from and out of alignment with the filling tube d and thereupon follows a cleaning of the hopper. This comprises several cleansing phases including the washing out with water and steam before the hopper is brought again into ,filling position for a subsequent batch of corn. When the empty hopper 0 therefore is moved back over the perforated or sieve plate the holes in the plate are clean and it is in sterile condition.

The empty hopper is now aligned and is directly over the perforated plate 0 and the pin cleaning device g is in its lowered or normal position. Water is next brought into the hopper from the top and washes down the sides and through the plate perforations. Any particles of corn which do not fiow through the sieve openings are left on top of the sieve plate. This leaves the hopper and the hopper bottom clean although there may be some corn particles left on top of the bottom plate as just mentioned. The wash-,

ing of the hopper is illustrated in Fig. 9.

The water drains off and then steam is caused to circulate through the hopper and plate perforations being brought in from the bottom and vented at the top to atmosphere. This conditions the hopper for receipt of its next charge of corn. Description of operations upon the charge of corn in the filling tube d will now be resumed.

Simultaneously with the removal of the hopper a from its alignment with the filling tube (1 a filling and discharge plunger h is moved over the top of the filling tube. It is brought into alignment with the filling tube at the same time that the hopper aligns with its perforated or sieve plate 0. The filling tube, it will be recalled, contains its charge of corn through which steam is flowing from the perforations of the slide j which at that time forms the bottom of the tube.

While the steam continues to enter the corn The upper end of the mouth of the tube is slightly flared and the rising steam escapes around' the lower end of the plunger and enters the middle chamber i. At about the same time that the plunger comes into the flared end oi the tube the steam pressure is increased. Con- 'tinuing the consideration of the canning of corn as. an example the increased steam pressure at this stage may amount to thirty pounds and with a corresponding temperature of 274 F. and this steam still escapes around the bottom of' the 75 culated through the Jack Th s Ir n the plunger and entersthe middle chamber 1'. Provision is made for venting the chamber at this time so that there is a circulation of steam through the corn mass and any air that might have entered chamber 1 is removed.

The plunger carries a piston ring near its lower end and when the plunger moves far enough into the tube this ring passes below the bottom of the flare of the mouth of the tube and enters the straight bore. The fit of the piston ringwithin the straight bore of the tube provides a steam seal blocking off any escape of the steam at that time from the top of the tube.

In other words, the filling tube with its charge of corn is cut off from the middle chamber 1', but this sealing does not take place until a higher temperature and pressure of steam is introduced into the fillingtube. Steam at fifty pounds pressure and at a temperature of 297 F. starts entering the corn mass before the tube is sealed by the plunger. The corn oonfinedwithin the tube is now subjected to several steps or stages of increasing temperature all taking place within the sealed off tube, the steam entering from below through the perforations of the tube slide f.

Th first of these sealed-off sterilization steps has already begun, as just described, by steam at the pressure of fifty pounds and temperature of 297 F. This continues for a few seconds and then the corn within the tube is subjected to more steam pressure and higher temperature, 1. e., the steam entering the corn is at sixty pounds pressure and at a temperature of 307 F. Following a few seconds of this treatment the steam pressure is further increased, for example to sixty five pounds of pressure and at 312 F. temperature. These sterilization steps at increasing pressures and temperatures complete the sterilization of the product in a remarkably short time.

Preferably throughout all. of the sterilization steps just mentioned and also at and immediately following the filling of the corn into the filling tube, the latter is heated from the exterior, this being in addition to the heating by means of the live steam entering directly into the corn through the perforations of the slide 1. To efiect this exterior heating the tube 11 is surrounded by a space which constitutes a tube jacket 1'.

Through this space steam is circulated at temperatures and under pressures which correspond at any given time in the sterilizing steps to the temperature and pressure within the filling tube. The walls of the tube are relatively thin and this provision of having the same temperature on both sides of the tube wall prevents heat losses by conduction and insures quicker sterilization action.

From the time the plunger h seals off the top of the heating tube and continuing throughout the different stages of sterilization of the corn within the sealed tube steam is introduced in the middle chamber 1 and at the beginning the chamber is rapidly brought to fifty pounds of pressure and the entering steam is then at a temperature of 297 F. This high pressure will be maintained in the chamber until after the sterilization of the corn is completed. I

At the end of the high pressure and high temperature sterilizing period the steam entering into the product from the bottom of the filling tube 4 is cut oil. The steam which has been circulated through the tube .jacket 7' during this period is also cut off and cold water is then cirtemperature in the corn and condensation of steam within the corn mass immediately follows.

While circulation of cold water through the jacket continues to reduce the temperature of the corn in the tube conditions are immediately established for draining off the condensation. This drainage is done in two stages, the first stage by way of a pressure relief valve which is set at forty five pounds pressure. At the end of the first drainage step the corn mass will have dropped in temperature to about 291 F. and there will be forty five pounds pressure within the tube.

Circulation of cooling water within the tube jacket continues and the temperature of the corn is further lowered. In this second cooling stage condensation resulting from the drop in temperature of the corn will be drained from the tube, this time by way of a twenty pound pressure relief valve.

Near the end of this stage of cooling the perforated slide 1 closes 'so that perforations are no longer at the bottom of the tube. This action also cuts off further drainage, the corn mass now having been reduced in temperature to about 260 F. and with a pressure of twenty pounds.

Following the closing of the slide circulation of water through the tube jacket continues and the corn within the tube continues to give 'off heat. As the corn comes below a temperature "of 212 F. a negative pressure is generated within the tube. The tube is sealed at both top and bottom at this time and is further protected against contamination as will be hereinafter fully described.

At the end of the cooling period the sterilized corn is ready for the can. The can into which.

the sterilized batch of corn is to be placed has already been sterilized and consideration will now be given to this phase of the process.

The empty open top cans designated by the letter R: (Fig. 1) after passing through an outer entrance valve 1 are introduced into a can sterilizer m wherein steam under proper pressure and temperature sterilizes all surfaces of the can both inside and out. An inner can valve n next transfers the sterile empty can from the can sterilizer and places it into a filling, brining and closing chamber 0.

Saturated steam at low pressure, for example at one pound, or sterile gas at the same pressure may fill the chamber. In some instances the chamber may be vacuumized to a high degree of vacuum, it being necessary to protect the food in the heating tube when under vacuum from any bacterial contamination. It is while in this chamber that the sterile can'r'eceivesthe charge of sterilized corn which has just completed its cooling cycle.

As best shown in Fig. 2 the sterile can moves beneath the bottom end of the filling tube and when in proper position the slide member 1 moves back so as to fully open the bottom of the tube by aligning a discharge opening therewith. Thereupon the corn is pushed down into the can by descent of the plunger h.

The filled can with its charge of sterilized corn and still in the chamber may next pass to a briner 12 if the product is to be brined, as in the case of corn. The briner p is hermetically enclosed within the chamber 0..

After receiving the desired brine the can is hermetically sealed while still in the chamber 0. Any suitable seaming or closing mechanism may be used for this purpose, the letter q designating such a device (Fig. 1).

Can covers for closing the cans must be first sterilized and then introduced into the chamber 0 for the closing machine q. Such covers are fed in any suitable manner, first through a sterilizing device 1- which is mounted in or adjacent to the chamber 0. Device r sterilizes the cover and the sterile cover thereupon enters the chamber 0. It is then brought into position on the filled can for the can closing or sealing operation, this being effected in any suitable manner.

The sealed can is then discharged from the chamber 0 without delay. In order to permit such a discharge without breaking the seal of the chamber 0' a discharge valve 8 may be used. In some instances the can may not be sufiiciently cooled when it leaves the chamber 0 and obviously further cooling may subsequently be had.

Reverting back to conditions affecting the perforated tube slide 1, it will be recalled that before the sterilized and cooled batch of corn within the filling tube d is ready for discharge into the sterilized can, the tube slide was moved to carry its perforations out of alignment with the bottom of the tube. Further movement now brings a discharge opening formed in the slide in alignment with the plunger h, (Fig. 2) followin which the corn is filled into the can. It is at such a time that the perforations of the slide are brought under and aligned with a. pin cleaning unit t which is constructed substantially the same as the pin cleaning device g.

Furthermore it is during the filling of the corn into the can and as the descending plunger h is traversing the filling tube d. that the perforations of the slide f are cleaned by the cleaning unit t. In this cleaning action sterile water and steam are forced through the holes. Then the pins of the unit are moved down into the periorations of the slide (Fig. 2). This forces out any food particles that may have lodged in the holes. This is followed by more washing by means of sterile water and steam. For this purpose the water and steam may be at 260 F. temperature. The water, condensate and fine food particles are then drained from the slide.

In the lowermost position of the plunger h, this being when the can It has received its full charge of corn, its bottom end acts as a. topper for the can and in this position extends through the opening 0f the tube slide 1. The plunger then moves up out of the slide opening and at the same time the tube, plunger and slide are moved away from the filled can.

Sterile water which may be heated if desired, is now forced-through the slid opening and into the empty filling tube under a' suitable pressure,

which may be .for example twenty pounds. This water fills the tube and fiows against the bottom of the plunger while it is still ascending, as shown in Fig. 10.

Just before the piston ring carried by the plunger it passes into the flared mouth at the top of the filling tube the flow of water is out off but th rising plunger continues its ascent. As the plunger opens up the top of the fillins tube the sterile water in the middle chamber 1', which is under a steam pressure of fifty pounds. forces its way into the tube and at the same time the bottom of the tube is connected with drainage (Fig. 11). Accordingly .the' tube isemptied and all of the hot water in the middle chamber is evacuated by way of the tube and drainage.

During the last portion or the draining operaa chamber.

,over an idler sprocket 34.

azaaceo tion, the perforated slide j is moved to bring its perforations in alignment with the bottom of the The steam Which'has been supplied to the middle chamber 11 under its fifty pounds of pressure is now out off and as the filling-tube is finally emptied the pressure of the steam with in the chamber 71 is relieved, the tube and the perforated slide being thus left in a sterile con dition and ready to receive its hopper full ofcorn. This completes the cycle ofopera'tion.

Consideration will now chanical features of the apparatus herein illustrated for the practice of theinvention, In a broad sense the apparatus comprises a stationary fram 2| (Figs. 1 and'2); which for the most part is cylindrical in shape and a cylindrical movable housing 22 mounted on the frame. These parts are somewhat massive being adapted for the canning of corn with a production capacity of about 150 or product per minute. v

The movable housing carries som eightyslide units 23 each of which is radially disposed and each is in some stage or step of the treatment at any particular position throughout its rotation around the frame 2|. Each slide unit may be considered as a compound: or double unit for each carries one hopper w and one filling plunger It and in addition to'the rotative movement with an associated filling tube (1 is movable relative to the tube. At any one time therefore a unit is functioning in its duplex capacity, some step in the treatment taking place as to the hopper and another step as to the filling tube. I

The machine frame 2| is extended at one side into a rectangular section 24 and it is in this section that the empty cans k are introduced into the machineand after filling are sealed and then discharged therefrom. The walls of the frame section 24 provide valve seats for the outer entrance valve 1 (Figf'l) the'can sterilizer m and the inner or chamber valve n.

160 cans of fully treated '10 be given to the me- 1 and 2) which at its bottom zonta-l wall 42. In its section '28 the frame wall 42 provides the'fioor sealing chamber 0 and this wall carries a horizontal runway 43 (Fig. 2) along: which the cans travel when advanced by the chain 32. On the opposite or return run the chain is carried in.

in the wall M. It is also the wall a groove it cut 42 that carries their shafts. I

Just above the wall it at the base of the cylindrical wall M a spaced horizontal wall is an in tegral part of the frame and in the section it of the frame carries a chamber top plate 45 the outer edge of which is mounted on top of an outside wall part 46. This top plate in the front or the machine and parts of the wall 42 are flush on their upper surfaces and provide support for the the conveyor sprockets 33, 34 and movable housing 22 which surrounds the cylindrical frame part ll. The top plate also forms the roof for the chamber 0 and by means of suitablepacking dl.

The cylindrical wall d! carries at formed with a middle 'web Hand a vertically disposed peripheral wall 5 3. It is inside of the member 5! that the reservoir b isdisposed(-l' *igs.

The reservoir 12 is oval in plan and dips down toward the outer side at its zone of contact with the peripheral wall. This bottom directs any food. particles passing through the A can entrance chute 26 directs the empty open top cans k into a pocket of the rotary valve 1-. The valve Z introduces the can into a pocket of a rotatable turret 21 which islocated in the sealed chamber of-the sterilizer. While the cans are carried around through the sterilizer by the rotating turret 21 they are subjected to high temperature steam which circulates within the sterilizer chamber. This steam may be introduced into the chamber by an inlet pipe 28 and removal of steam and condensate maybe made by way of an outlet pipe'29. The sterilizer m may be of any suitable construction and as its construction features form no part of theinvention further description is considered unnecessary.

The sterilized can is is removed from the pocket of turret 21 andis transferred by the rotating valve it into the filling, brining and closingchamber 0. The valve 11. places the can between spaced prongs'3l of a horizontally disposed con tinuously movable endless conveyor chain 32. This chain operates over a drive sprocket 33 and above the chain as it moves around the idler sprocket and is then kept ina proper line of travel, i. e., over the chain by an inner guide bar 35 and an outer guide'rail'36. The can is thus advanced between the sprockets 34, 33 and at one position in its travel it receives its fill of sterilized corn. This will be fully explainecl'at the proper time.

The stationary frame =2! is formed with a central, cylindrical vertically disposed wall 4i (Figs.

The can is placedreservoir to an elongated slotted opening 56 cut through the bottom. The reservoirshell is held in fixed position by straps posed on'the upper edge of the'shell part 54 and through the cover, a supply of the raw product may be introduced in any suitable manner'to replenish the supply of product in the reservoir.

The movable housing 22" comprises a bottom horizontal web 6| (Fig. 2) from vertically disposed circular lower wallfiz (see also Fig. l) The wall 621s enlarged at spaced intervals to provide the surrounding tube jackets, and

this wall also carries the filling tubes 12. There" are thus eighty of these tubes with their. jackets 7'.

The lower web 6| carries a ring gear-63' and it is through this medium that the movable housing and all parts carried thereby are continually rotated. A drive pinion 64 meshes with the gear and provides for proper transmission of the necessary rotative power.

'At the top, the wall 62 merges into an annular intermediate section 65 wherein is located the J slide units 23. This intermediate section is cut provide steam tight. joints.

across in wall pockets 66 having parallel sides and adjacent pockets are separated by a spacer wall 61. Each slide unit has free radial movement within its pocket but its sliding surfaces There is a middle chamber i for each unit and each chamber is located in part in its associated pocket 66.

The top wall of the intermediate sectionis in horizontal alignment with'the lower face of the stationary web. member 52 andtheslide unit 23 has a steam tight sliding fit at this'place. At its outer endthe pockets 66 are sealed by a horizontalflange ll of an upper annular.housing memberllz. The periphery of the flange ii ,is boltedtight'to' the intermediate section and is made steam tight by a packing 13.

merges into a hori for the filling, brining and is tightly sealed '1 its top a" bowl like member 5| (Figs. 1 and 2)Y which is isformed as a surrounding shell 5 which contacts with.

frame part 24. A sloping bottom 55 of the reservoirshell 51. A cover 58 is diswhich extends a The housing 12 confines the upper chamber e, the stationary wall part 53 providing the inner boundary of the chamber. Thus it will be evident that there is only one u per chamber e for all of the slide units 23 and this chamber is annular in shape and surrounds the stationary inner bowl like member A ring cover 14 is bolted at its outer periphery to the top of the housing I2 and at its inner rim has a sliding fit on a flange I5 formed at the top of the wall 53. A packing strip I6 makes this sliding fit steam tight. A check valve or steam vent 11 (Fig. 7) may be placed in the ring cover I4 to prevent too great an accumulation of pressure in the chamber e. The maximum pressure setting of the check valve may be one pound, for example.

Each slide unit 23 (Figs. 1 and 2) consists of a rectangular block 8| the sides and bottom of which are at all times sealed in a sliding steam fit within the parallel side walls and the bottom wall of the pocket 66 in which the unit operates. In a similar manner the top of the block has a close sliding steam fit with the under surface of the central web 52 at its inner end and with the under surface of the flange II of the housing I2 at its outer end.

Each block 8| centrally of its radial dimension is cut through from top to bottom with a vertically extending opening 82 which in shape is as the frustrum of an inverted cone. This opening constitutes the hopper a and its volume therefore, in this present embodiment, is sufficient to hold a single can batch of the product.

Just back of the opening 82 a vertical bore 83 is out through the block and the filling plunger h is slidably carried in the bore. The inner end of the block is recessed at 84 and a vertical bore 85 passes through a part of the block and extends from the bottom of the recess to the bottom face of the block. The bore 85 is used in cleaning out the perforated sieve plate 0 as will be hereinafter fully explained.

The outer end of the block 8| is also recessed as at 86 and this recess forms part of the middle chamber 1'. It extends inwardly and surrounds the plunger h as clearly shown in the drawings. The plunger h is vertically movable in the bore 83 and during such movement is held against rotation on its own axis by a feather 81 which is held in the block and which projects within a featherway formed in the inner side of the plunger.

Plunger h is raised and lowered within its bore 83 by can action and for this purpose carries a cam roller 88 rotatably mounted on a stud 89 threadedly engaged in the top of the plunger. This ca'm roller traverses a cam groove 99 cut in the peripheral wall 53 as the movable housing 22 and parts carried thereby rotate around the stationary frame 2I.

The block 8| is moved from an inner hopper filling position (Fig. 8) to a hopper discharge position shown in Fig. 7. This movement is effected by a cam groove 9| cut in the bottom surface of the stationary web 52. A cam roller 92 is rotatably mounted on a stud 93 and the latter is screwed into the block 8| at its inner end. As the slide units 23 are carried around by the continuously moving housing 22 the roller 92 traverses the cam track and is moved in and out in proper time.

Each block 8| is in its inner position when it passes beneath the reservoir b and its hopper opening 82 moves along and under the slotted opening 56 in the reservoir bottom 55. The fillis also directly over the perforated sieve plate 0.

Each sieve plate comprises a spaced double web memberwhich is set into a vertical bore 94 formed in the intermediate housing section 65 just below the bottom of the pocket 66. Its upper web is flush with the bottom floor of the pocket. The web 95 is perforated and these perforations align with similar perforations formed in a lower web 96. The space between the webs 95, 96 connects with the outer end of a horizontal channel 91 which extends inwardly to the stationary wall 4| of the stationary frame 2|.

It is through the channel 91 that the low pressure steam is brought into the space between the perforated web sections 95, 96 and the steam escaping up through the holes of the web 95 passes on up into and through the hopper a and on up through the corn in the reservoir b as has already been described.

The pin cleaning device g is also located in the bore 94 and includes a head 98 on which is carried cleaning pins 99. When in non-clean ing position, as during filling of the hopper the head is at the bottom of the bore 94 and the tops of the pins are flush with the top surface of the lower web 96. The head 98 is formed with a stem I9I which extends down through the'frame and into a space I92 located just inside of the wall 62.

A lever I93 is located in the space and is pivoted at I94 on a depending bracket I95 which extends down from the housing part 65. The

outer end of the lever is slotted as at I96 and this provides a loose connection for a pin I91 carried on the stem I9I.

The inner end of lever I93 carries a cam roller I98 which operates in a cam groove I99 formed in the peripheral surface of the stationary cylindrical wall 4|. As the movable housing and parts carried thereby rotate around the stationary central frame the cam roller traverses its cam track and the lever is rocked on its pivot to raise the pins 99 at the proper time to clean out the perforations in the web 95.

Consideration will now be given to the perforated tube slide f which is an associated part of each filling tube d and reference should be had to Figs. 1, 2 and 3. Each tubeslide is moved across the top plate 45 in'front and across the horizontal frame wall 42 at the'sides and .rear as the movable housing 22 turns around its stationary frame 2|. The under face of the horizontal web 9| is cut into by rectangular slots III there being one slot for each rectangular slot is radially disposed and is centrally located as to the longitudinal center of the tube. Such a slot provided a close fitting sliding seat for the tube slide 1.

Each tube slide 1' is pierced through intermediate its longitudinal axis with perforations H2 and near its outer end with a circular opening II3. This slide has an outer position- (Fig. 8) where its perforations II2 are aligned beneath the filling tube 11. It also has an inner position (Fig. 2) where its circular opening I I3 is aligned beneath the filling tube 02. An-intermediate position shuts off the bottom of the filling tube I (Fig. 10).

Slide f is cam controlled and for this purfilling tube d. Each with an annular channel azaaeao pose carries at its inner end a cam. roller 4 which is mounted on a stud, I It threadedly secured to and depending beneath the slide. The cam roller lid operates in a cam groove IIti (see also Fig. 3) out in the upper surface of the top plate 45 and in the frame wall 42. As the movable housing 22 revolvesaround its stationary frame it roller H4 traverses-the cam'track H6 and the slide is thus moved into its difierent positions Just back of orinwardly from the filling tube d is located the tube slide-pin cleaning unit it. This unit is of the same construction as the pin cleaning device 9 already explained and-is just below and in vertical alignment therewith. The unit is contained within a vertical bore IN and comprises aperforated web member I22 which is set into the bore and with its lowersurface flush with the top of the slide 3'. Cleaning pins I23 project down from a head I24 also contained within the bore IN. The perforations in the web I22 act as guides for the pins which are adapted to be lowered through the perforations I I2 of the slide when the latter is in its inner position.

The head IE4 is formed with a stem I25 which extends up and into the recess W2. A lever I28 is located in thisrecess and is pivoted at I21 on the bracket I05. Its outer end is slotted for a loose connection with a pin I28 carried by the stem S25 and its inner end carries a cam roller I29. As the movable housing22 and parts carried thereby wall 49 the cam revolve around the stationary roller I29 traverses a cam track I3I' cut in the periphery of the wall and in this manner the pin cleaning unit g receives its proper actuation.

Having fully described the principal parts of the apparatus, attention will now be directed to the functioning of these parts and to the application of steam and water in the diflerent places through an opening in the frame wall tent of channel. I32v and also shows. that the low pressure steam ply pipel33'.

After passingv contains its charge of. com, ing passed beyond the reservoir slot the hopper then havbegins the period of steam treatment of the com where needed. The complete'cycle of operations will again be briefly mentioned and some idea of relative time should be understood that by way of illustration only of product being treated will largely dictate exact time values. Even in the treatment of the same product, such as corn, the variety, freshness'and other characteristics will affect the timing of the difierent'steps in its treatment.

In the plan sections of Figs. 1, 3, 4, 5 and 6 where the relative time values can best be seen, the same positions throughout the cycle where a change in operation occurs are indicated in the figures by the same designated and located radial dot and dash lines. V

For the description that follows the filling of the hopper d is arbitrarily chosen as a point of beginning. The same slide unit 23 will be followed throughout its complete cycle which means for two revolutions of themovaiolefhousing on the stationary frame. When this slide unit moving in a clockwise direction (Fig. 1) passes the radial position H the filling of 'thelhopper a with corn from the reservoir 1) begins; This filling continues until position b-b is passed. Fig. 8 shows this step. It takes two seconds to make the fill.

It will be recalled that low pressure steam is passing into the'hopper v tion in the web 95 of the sieve plate 0, the steam entering th'roughthe channel 91. The-inner end of this channel .at this time is'in communication I32 cutin the periphery Fig. 5 shows the-exsuch time figures are of the cylindrical wall II.

values will be set forth. 'It' inasmuch'as the kind by way ofzthe perfora-' tube that the hop r teen seconds formed in the under face of the web 52.

movement. 23 is'shown in Fig. 7.

while inthe hopper and this continues for nineor .until the filledv hopper reaches the'position k.k (Fig.5) Ten pounds pressure of steam at a temperature of 240 F. may be used. for this treatment and this. steam is introduced through the, perforated web 95 (Fig. 2) into the hopper by way of the channel 91. The inner end of channel 81, during the movement of the hopper from position bb t0 kk,,is in communicationwith a-channe1-I35 cut in the periphery of theeylindrical wall M. The channel I35 may be supplied with steamby way of spaced supply pipes. I36 (see alsoFig. 5).

. Fig. 2 showsthis steam treating operation and it will beobserved that the "steam passing up through the corn enters an annular channel I31 Fig. 6 I31 extends from position I31 emptied by a shows that the channel bb to position kk. Channel transverse port Thus circulation of steam is maintained by entering through the pipes I36 and exhausting by way of pipe I39.

. Throughout this steam treatment the slide unit 23 with itsv hopper a is in its innerposition, being so held by the cam track 9|. After passing the position We therefore steamis cut off from the bottom of the hopper which now with its charge of corn moves the course The outer position of the slide unit When this movement takes place the plunger his in its highest position the cam groove 90 at this place'being at its highest point. When the slide unit moves out it takes away the cam roller 88 from its cam groove 90,

as shown in Fig. '7. In order to keep the plunger h in its raised position so that it can be returned to the cam groove, a spring pressed detent I4I is used. The detentis located in the slide block and its inner end engages in a groove I42 cut in feather 81 and this the plunger opposite the maintains the plunger in raised position.

Emptying of the corn next follows and as the corn discharges from the hopper a into the filling tube at (Fig. '7) steam passes up through the corn in both tube and hopper and passes on into the upper chamber c. This steam, pressure of ten pounds and at a temperature of 240 F.;in the tube, enters through the perforations In in' the tube slide ,f the steam coming through a pipe.,l45, and apassageway I46 which leads into an annularchannel horizontal framewall 42 tent'of the channel I41. trom hopper a to tubefb. cc'uisunries only'about one and a half secondsreturned to its inner position." I

It. is while 'theslide unit is in outer position and during transfer of thecorn from hopper to sieve plate 0 is cleaned. '7 whi'ch also shows the I41, formed in the This is'shown in Fig. cleaning pins 99 being foration of the web 95. Before'and immediately after steam and hot water-"flow 'in between the web'sQB, 96 by way of the ch'ahneit'i which at this time passes i communication with a channel I5I formed in the stationary wall 4I. Water is fed to-the channel by sup-. the position the hopper 56. Now

I38 which leads into a pipe I39.

to itsouter position. Fig. 6 shows of the cam track-9lthat effects thiswhich is at a ig.3 shows the ex- The transfer of corn Then theslid'e' unit is pushed through the per and steam are brought into channel I5I by a pipe I52 and a passageway I53. The drainage, washing up through the opening 85 in the slide block 5| passes through the recess 54 and through the pocket 55 and out through a channel I54 formed in the wall 4| and thence through a passage I55 connecting with a pipe I55. Fig. 5 shows the extent and relative positions of the channels I5I and I54. The position I-I shows where this washing step is completed although the drainage by way of channel I54 may continue beyond that position.

The slide unit 23 is returned to its inner position during the travel from position I-I to position mm (Fig. 6) and the empty hopper a again comes to rest over the cleaned sieve plate c. Two things now take place, the empty hopper is washed out and the filling tube 41 with its charge of corn begins its steam treatments. The cleaning of the hopper a will first be followed and each operation covering the travel of the same from position mm back to the point of beginning aa will be noted before returning to position mm for consideration of the filling tube d.

Upon passing the position mm water is introduced into the hopper a from the top as illustrated in Fig. 9. From position mm to 1m (Fig. 6) this water comes from a pipe I5I, passes through a sinuous passageway I52 formed in the stationary wall 4| and web 52 and discharges into an elongated channel I53 cut into the under face of the web 52. An oblong perforated spray head I64 is set into the bottom of the channel and this spreads the water in a series of jets which strike against the walls of the hopper a and wash down any food particles which may be left in the hopper. The water and fine drainings pass out through the perforations'in the web 55 of the sieve plate and are carried out by way of the channel 91.

When the hopper is subjected to the spray of water from the perforated spray head I54 it is in heated condition and if the spray water used is above a normal boiling temperature the drainage will begin immediately since the pressure in the hopper will be above atmospheric pressure. If, however, cold water or water below the normal boiling temperature is used vacuum will be formed in the hoppe" and drainage of the spray water will be momentarily delayed until such a time as the vacuum can be dissipated.

At this time the inner end of the channel 51 is in communication with a channel I55 cut in the periphery of the frame wall II. Channel I 35 is connected by a bore I55 to a discharge pipe I 51. The bore and pipe are also in the wall II. Fig. hows that the channel I55 extends from position mm to a point about half way between positions nn and 0-0. In this washing period the water flows into the hopper for about two seconds and the total drainage period may be about three seconds. Any food particles too big to pass through the perforations of the sieve plate c remain at the bottom of the hopper.

The full drainage period of three seconds will obtain where hot water is used in the spray head and the drainage water will then be discharged from the hopper as soon as the channels 51 and I55 are connected. Where cold water is used, as explained above, it is first necessary to dissipate the vacuum in the chamber and this is done by air entering from below by way of the discharge pipe I51, bore I55 and channel I55. Obviously the time required for breaking the vacuum, however brief, will shorten the drainage period as sug ested.

The water is cut off upon the slide unit 23 passing the position n-n but drainage continues since the channel I55 extends beyond that position, as already explained. This further drainage, following the cutting off of the water from above the hopper, is made possible by venting of the hopper from above. This venting is in effect during the passage of the hopper a from position nn to a-a which consumes about four seconds. About one second of this time'is consumed by passage of the hopper from the position n-n to the termination of the drainage channel I55.

As shown in Fig. 6 the hopper immediately upon passing position n--n moves under a channel I1I formed in the web 52. A passage I12 formed in the web connects this channel with a vent pipe I13. No cross section is shown of the hopper and the associated parts when it is passing beneath the channel "I but it will be understood that this channel corresponds in structural details to the channel I31-and the passage I12 and pipe I13 are the counterparts mechanically of the passage I33 and pipe I35. The entrance of air into the hopper by way of the vent channel HI and vent pipe I13 insures complete drainage of the wash water.

Immediately after the slide unit 23 passes the end of the drainage channel I55, the end of channel 51 registers with the low pressure steam channel I32 and steam entering through the perforations of sieve plate 0 in the bottom of the hopper prepares it for its next charge of corn. This steam escapes through the vent channel I1 I, passage I12 and vent pipe I13 until the position 0-41 is reached. This drives out the air from the hopper. Thus one revolution of the slide unit 23 is completed with the hopper u again reaching position H. v

Returning to the filling tube (1 with its charge of corn which is passing into the first stage of steam treatment therein, with the tube at this time advancing from the position 111-111 to the position n-n. At this time the plunger h under the action of the track 55 moves down into the open flared top of the filling tube. When the slide unit 23 was returned to its inner position the cam roller 53 carried on top of the plunger h was again inserted into the cam groove 55. In its travel from m-m to nn, which requires about two seconds, the'plunger is moved into the flared mouth of the tube.

The plunger carries a piston ring I15 (Fig. 7) and this ring at the time the moving slide unit reaches the position 11-11 is just above the straight bore of the filling tube. This leaves about $4 of an inch clearance around and beneath the piston ring to permit escape of the .steam which is entering the bottom of the filling tube through the perforations of the tube slide f. This position of the plunger is not illustrated in detailed section in any of the figures of the drawings.

The perforations at the bottom of the filling tube which are in the tube slide pass over a channel I15 (Fig. 3) which is formed in the upper surface of the frame part 42. This channel is connected with a passageway I11 cut in the frame wall which communicates with a steam pipe I15. The steam in the tube supplied by the pipe I18 is under a pressure of thirty pounds and at a temperature of 2'14 degrees and is maintained for about two seconds. This insures that the higher steam pressure entering into the filling tube and passing through the corn mass therein escapes through the small clearance opening just beneath just short of this half way point. After the half way point is passed no more steam enters the middle chamber i from the filling tube d since the latter is then closed by the plunger h.

Immediately. following, however, high pressure steam is introduced into the middle chamber, this steam being at a pressure of fifty two pounds and at a temperature of 300 F. Putting the middle chamber under this high pressure is done in the following manner. The inner end of the passageway I19, just after passing the point at which the venting of the filling tube terminates,

the outer end of the pocket 68. The walls of this pocket surround in part the chamber i.

The inner end of the passageway I19 as it moves between positions ZZ and half way between n--n and o o communicates with an annular peripheral channel I88 (see also Fig. 13) cut in the wall 4| of the stationary frame. This is a vent channel 'which may open up to the inside of the wall 4| and in this way the steam, with any air or other gas entering the middle chamber from the filling tube, is vented.

Provision is madefor maintaining a pressure 'of thirty pounds of steam with its corresponding temperature of 2'74 F. within the jacket a surrounding the filling tube (1 during passage of the parts from mm to nn. For this purpose steam enters the jacket through a passageway I 8| (shown in Fig. 8) cut through the lower part of the intermediate frame section 85. The passageway I8I during the movement of the slide unit between positions mm and nn combetween mm and n-n the inner end of the passageway I85 communicates witha peripheral channel I86 cut in the outer wall of the cylindrical frame section 4| (see also-Fig. 4). This channel I86 is connected to a pipe I88 by means of which the steam condensate is led away from the tube jacket.

During. the next movement of the rotating housing relative to the stationaryframe, that is from position 1tn to oo (Figs. 3 and 4) the steam pressure is increased in both the filling tube d and in its jacket 1'. At this time the perforations in the bottom'of the filling tube pass over a channel I9I (Fig. 3) which is connected by a passage I92 with. asteam pipe I93. This pipe delivers steam at a pressure of fifty pounds and at a temperature-of 297 F. and this condition obtains for about two seconds.

Up until about the half way point in this travel between these positions a part of the steam escapes through the clearance opening between the bottom of the piston ring I on the plunger h and the top of the cylindrical bore of the filling tube 6 but as this half way point is reached the plunger h is lowered sufficiently to enter its piston ring I15 into the cylindrical bore of the filling tube. thus blocking off any escape of steam from the top of the tube. I

Just before reaching this half way point the vent connection to the middle chamber is closed, Fig. 13 showing that the channel I88 terminates comes into communication with a peripheral channel I94 (Fig. 13) cut in the outer wall ofthe frame part 4|. Channel I94 extends over 270 or around the frame wall to the position 7ck.

Pipes I95 joinin with the channel I94 at different places introduce and maintain this high steam pressure in chamber 1' as long as the chamber is in communication with the channel I94 which is for about twenty two seconds During this same movement, 1. e., from nn to 00, steam in the jacket 1'" is also increased to a pressure of fifty pounds and with a temperature of 297 F: Fig. 4 illustrates this operation. During such movement the inner end of the .passage I8I communicates with a peripheral channel. I96 cut in the outer surface of the cylindrical stationary wall 4|. This channel is connected to a steam pipe I91 which delivers steam at the proper pressure and temperature to the upper part of the tube jacket 7'. At the same time the inner end of the passage I communicates with a peripheral channel I98 which is connected with a pipe I99, thus permitting escape of the'steam condensate from the tube jacket.

During the passage of the slide unit 23 between the position o-o and a-a sixty pounds of steam pressure is introduced into the closed filling tube 41 with its confined charge of corn, this being as before through the perforations at the bottom of the tube. At the same time a corresponding steam pressure is circulated through the jacket a' of the filling tube.

As illustrated in Fig. 3 the perforations at the bottom of the filling tube now pass over a channel 28I formed in the wall 42 which is connected by a passage 282 with a steam pipe 283. This pipe introduces steam into the closed tube at a 4 temperature is introduced into the top of the I jacket. At the same time the inner end of the passage I85 communicates with a peripheral channel 281 also cut in the frame wall and connected with a pipe 288. This steam at sixty pounds of pressure is held in the steam jacket while steam is introduced into the bottom end of the closed filling tube.

The slide un.it 23 has now reached its starting point and the description that follows relates to the second revolution of the slide unit and particularly is concerned with the treatment associated with the filling tube (1 as it makes its second revolution around the'stationary frame part of theapparatus.

In the passage between aa and 11-11 the perforations at the bottom of the filling tube d pass over a channel 2 (Fig. 3) which is connected bya passage 2l2 with a steam pipe 2|3. This pipe introduces steam into the bottom of the closed and filled tube (1 at a pressure of sixty five pounds and at a, temperature of 312 F. This is the last stage of the sterilizing of the food within the filling tube. At the same time the same temperature and pressure of steam circu lates through the jacket a surrounding the filling tube. This last stage of steam treatment consumes abouttwo seconds.

To obtain the proper circulation of steam in the steam jacket during this movement between the position a-a and b-.-b the inner end of the passage I8! communicates with a peripheral channel 2l5 formed in the outer surface of the wall 4! and which is connected with a steam pipe 216 by means of which steam at the desired pressure and temperature is supplied to the upper part of the jacket. At the same time the inner end of the passage I85 registers with a peripheral channel 2" (Figs. 4 and 8) formed in the outer wall of the frame member M. This channel is connected with a pipe 2l8 which allows for escape of steam condensate from the bottom of the tube jacket :i.

This completes the heating feature of the sterilizing operation and the next interval of time is concerned with the cooling of the product. Between the position 12-12 and -0 the perforations of the tube slide 1 at the bottom of the fill ing tube pass over a channel 22l (Fig. 3) which.

is connected by a passage 222 to a drain pipe 223 in which is located a relief valve 224. This relief valve is set at forty five pounds pressure and any pressure over that is relieved through the 4) cut in the outer surface of the wall 4| and.

which is connected to a cold water pipe 226. This introduces'cold water into the bottom of the tube jacket. At the same time the inner end of the passage l8l communicates with a peripheral channel 221 formed in the frame wall 4| and this latter channel connects with a discharge pipe .228. Circulation of cold water through the jacket from bottom to top continues through the various positions following the position bb until the position y-Q is reached so ,derstood, however, that cooling still continues since the cold water circulation through the jacket of the filling tube isuninterrupted.

The slide unit just after passing the position ee and with the bottom of the filling tube it closed by the slide 1 comes over a channel 24! (Fig. 3) which is cut in the upper face of the frame wall 42. This particular position of the parts is not illustrated in detail in the drawings. The channel.24l is connected by a passage 242 with a pipe 243.

Cooling of the corn mass within the tube d continues after the slide 1 closes the tube. This cooling of the product while still in the tube may be brought to such a point that a vacuum is created in the tube. The pipe 243 therefore may be connected to a source of vacuum which'is higher than any vacuum which may exist in the tube and in that event the channel 2 and the under side of the closed tube slide 1 will be brought under vacuum.

In some cases a sterile, non-condensible gas such as air or nitrogen may be supplied through the pipe 243 to fill the channel 24! under the closed tube slide f. Such sterile gas when used would preferably be at a slight pressure, for example, one pound. In still other cases it may be advisable to fill the channel 2 with saturated steam at a slight pressure.

The channel .24! functions as a protection to the food in the heated tube against bacterial contamination. Thisis an added insurance as it will be understood that the closed slide 1 substantially prevents the entrance of any bacteria into the product within the filling tube d. g

The channel 2 terminates just short of posi tion ,f-i so that when the slide unit reaches that position all communication with the under side of the tube slide 1 is terminated. In the passage of the slide unit from ,f-f to g-g some cooling will take place until the termination of the total cooling period of twelve seconds mentioned above.

Th corn is now approaching the filling stage when it will be filled into the empty sterile can being conducted through the chamber 0 by the conveyor chain 132.

As the slide unit passes from ,f to g-g the cam track IIB (Fig. 3) veers inwardly so that the tube slide 1 is brought from the closed position shown in Fig. 10 to the filling position shown in that cooling of the corn mass within the filling tube continues during this time which is about twelve seconds.

As the perforations at the bottom of the filling tube pass between position 0'c and position ee they connect with a channel 23l (Fig. 3) which is formed in the frame part 42 and this channel connects by a passage 232 with a drain pipe 233 in which is located a relief valve 234. The relief valve 234 is set at twenty pounds pressure and all pressures over that amount are allowed to dissipate through :the relief valve and liquid continues to escape from the tube d. This relief phase lasts for about three seconds.

Prior to reaching the position ee the slide 1' is moved to close ofl the bottom of the filling tube d. This is shown in Fig. 10. This is done by the cam track I I6 which as illustrated in Fig.

Fig. 2. In this latter positionthe opening' H3 formed in the tube slide f is brought in register beneath a'slot 244 (see also-Fig. 3) 'cut in ,the

top plate 45 just over the conveyor chain and as the slide unit passes from positions y-g to hh the cam track acting upon the plunger cam roller 59 forces the plunger down through the filling tube it, this action forcing the charge of corn, which is now fully sterilized and sumciently cooled, into the can 'as itpasses' along its straight lineof travel. Fig. 2 of the drawings shows this filling step well advanced over half of the com having been at that time discharged into the can. The total filling time is about two seconds.-.

The filled can still being conveyed by the chain 32 is then passed under the briner p (Fig, 1) and end of the tube which takes about" hereaiter receives an end from the endsterllizer and can'and end are then sealed toegther by he double scanner 9. The chain'thereupon inroduces the now sealed and filled can into a locket of the discharge valve s which removes ;he' sealed can from the chamber and diszhargfes it into a suitable place of deposit which may be by a runway as shown. The chamber 0 is supplied with its st am or sterile gas by a supply pipe 2&5 (Fig. l) and circulation of may be obtained if desired by an exit pipe 248.

While the can is being filled (Fig. 2) the Pins i22 of the pin cleaning device t are inserted into theperiorations N2 of the tube slide f. Before and following this operation steam and water are caused to flow through the holes and the water is drained away. During this action which is just after the slide unit has passed position 9- the slide perforations pass over a channel 241 (Figs. 2 and 3) cut in the chamber top plate 45 and this channel extends nearly to the position h-h. It connects by a passage 248 with a drain pipe 249. Water passing through the perforation of the tube slide f is thus drained of! byway of the pipe 249.

The space above the tube slide and just beneath the web member 122 is always connected with a passage 25! (Fig. 2), The inner end of this passage divides into two branches and during travel of the slide unit between g--g and h-h, which consumes about two seconds, the end of the upper branch comes in communication with a peripheral channel 252 (see also Fig. 4) formed in the frame wall 4!. This channel connects with a steam pipe 253 by means of which steam, at about fifteen pounds pressure and at about 250 F. temperaturaentersthe space above the slide perforations 2. I

At the same time the lower branch of the passage 25l' comes .in communication with a pcripheral channel 254 also formed in the wall 4|. This channel is connected to a sterile water supply pipe 255. In this way sterile water is supplied for flushing the perforations of the tube slide 1.

As soon as the filling tube d has been emptied of its charge of corn it is ready for cleaning. As the slide unit reaches the position h-h the open at and the opening H3 of the tube aligned therewith, pass over a channel 261 (Fig. 3) which extends between positions ia-h and i--i. This channel 2$l is formed in the top. chamber wall 45 and is connected by a passage 252 to a sterile water supply pipe 263. As soon as theplunger h completes the filling of the can the plunger is immediately raised and as the plunger moves'upthrough the empty filling tube d sterile water coming through the pipe 263, passage 262 and channel 261, flows into the filling tube, this water in the tube and slide j, which is still rising following the bottom end of the plunger as it ascends."

At the same time, that is, during the passage of the slide unit between position h--h and t-i two seconds, sterile water is forced into the middle chamber i against the steam pressure of fifty-two pounds.- It will be recalled'that this steam pressure is maintained in the chamber throughout all of the preceding period following its first introductionby way of the channel its.

As illustrated in Fig. 12 a passageway 21! is formed in the spaced wall adjoining the slide unit 23 and the o'ter end of this passageway opens into the outer end the same brings it into communication with the middle chamber i. The inner end of the passageway 2' during this movement between positions h-h and t-i comes into communication with a pcripheral channel 212 (Fig. 13) which is joined with a water supply pipe 213. As long as the channel 212 is in communication with the inner end of the passageway 21| sterile water under suflicient pressure flows into the middle chamber 72 and this water covers over the exposed floor of the pocket 66. y

when the slide uni-t passes the position ii the open bottom of the slide tube, that is the opening I IS in the tube slide 1, passes over a channel 215 which connects with a drain pipe 216, It is at this time that the piston ring I15 on the rising plunger 11. reaches the top of the straight bore of the filling tube. As the plunger It continues to rise communication is made between the middle chamber 1' and the water filled tube d.

The sterile water which was forced into the filling tube from below and which followed the lower end of the rising plunger together with the sterile water which entered the middle chamber i by way of the passageway 211 now suddenly discharges through the filling tube, through the opening 3 in the tube slide 1 and out through shut oil from the v are also provided in the of the pocket 66 which 75 the channel 215 and pipe 216. This discharge is very rapid since the full fifty-two pounds of steam pressure within the chamber 1' above the water in the chamber is effective against the draining water. This drainage period continues about three seconds or until position k-7c is reached. It is at this later position also that the chamber steam pressure of fifty-two pounds is chamber, the slide ,unit at that time passing'beyond the end of the peripheral channel I94.

As the slide unit approaches the position k-k and while the draining period just mentioned is still going on, the tube slide f is moved from its full open position of Fig. 11 into the perforation position where its perforations H2 are brought into alignment with the bottom end of the open filling tube d.

Just after leaving position 70-10 the slide unit is moved from its inner position to the outer position, the plunger It just prior to such movement having been brought into its fully raised position and held .in place by the detent I as previously described.

Concentric steam channels 281 (Figs 2 and 3) stationary frame part in order. to further insure against any contamination of the various channels which have already been described as being formed in the upper surface of the horizontal wall 42 a'nd'in the upper surfaceof the cover plate 45 on which move the housing 22 and parts carried thereby. These channels protect against entrance of germs from outside of the structure or from the inside of the moving surface along the central frame wall 4|.

Channels 28! are relatively deepand extend as continuous concentric rings in, the stationary frame parts 42, 45. The outer of these channels is located near the periphery of the composite wall 42, and

are therefore outside of the frame channels and passages previously mentioned. The inner channel is inside. ofsuch frame channels.

The two channels 28! are joined together at position 71-11 by a cross'groove'wi. This cross groove gives added protection for the filling zone. It especially protects the tube slide 1 as it moves from the can filling zone between g'-y 

